Self-regenerating particulate trap systems for emissions and methods thereof

ABSTRACT

A method and system for treating emissions includes charging particles in an exhaust stream, producing one or more radicals, and oxidizing at least a portion of the charged particles with at least a portion of the produced radicals. At least a portion of the charged particles in the exhaust stream are then attracted on at least one attraction surface which is one of oppositely charged from the charged particles and grounded. The attracted particles are oxidized with another portion of the one or more produced radicals to self regenerate the at least one attraction surface. Downstream from where the attracted particles are oxidized, at least a portion of one or more first compounds in the exhaust stream are converted to one or more second compounds downstream from the attracting. Additionally, at least a portion of any remaining charged particles are oxidized into one or more gases.

This application is a divisional of U.S. patent application Ser. No. 11/480,059, filed Jun. 30, 2006, which claims the benefit of U.S. Provisional Patent Application Ser. No. 60/696,978, filed Jul. 6, 2005, which is hereby incorporated by reference in its entirety.

FIELD OF THE INVENTION

The present invention generally relates to emissions treatment systems and methods thereof and, more particularly, to a self regenerating particulate trap system for one or more emissions and methods thereof.

BACKGROUND

There is a growing demand for energy usage in the United States, primarily due to increasing economic activity. This increasing demand for energy is being met by pursuing increased power generation. Unfortunately, this increase in power generation is resulting in the generation of over 160,000 tons of particulate emissions per year in the United States polluting the air.

Without significant new controls and treatments of emissions, millions of individuals will continue to breathe air polluted by these particulate emissions. Additionally, these emissions will continue to cause damage to environment in the form of acid rain and smog. Significant reductions in emissions of nitrogen oxides (NOx), particulate matter, nonmethane hydrocarbons, carbon monoxide, sulfur dioxide, and other toxins would result in substantial benefits to both the public health and the environment.

At the present time a device that is robust, efficient, durable, packagable, and maintenance-free is not available for elimination of particulate matter. For diesel engines in particular, several devices have been designed to combat the problem of particulate emissions. Most of these devices use different filtration technologies with either thermal regeneration capabilities or manually replaceable filtration media. The problem with these filtration devices is that they quickly clog and increase the exhaust backpressure thus negatively affecting efficiency and performance. In addition thermal regeneration requires vast amounts of energy and produces very high temperatures.

As discussed below, other technologies available for separating particulate matter from a gas stream have been investigated. For example, non-thermal plasma-assisted catalytic reduction of exhaust gases using a corona discharge have been studied and reported in the literature. J. A. Ekchian, E. N. Balles, D. L. Christeller, J. S. Cowart, and W. D. Fuller, “Use of Non-Thermal Plasma Generated by a Corona Discharge Device to Improve the Efficiency of Three-Way Catalyst”, which is herein incorporated by reference in its entirety, disclosed testing on the use of a corona discharge device for the reduction of HC, CO, and NOx in tailpipe emissions in conjunction with a three-way automotive catalyst and reported significant improvements.

Additionally, M. B. Penetrante, R. M. Brusasco, B. T. Merritt, W. J. Pitz and G. E. Wogtlin, “Feasibility of Plasma Aftertreatment for Simultaneous Control of NOx and Particulates”. SAE Paper 1999-01-3637 (1999)”, which is herein incorporated by reference in its entirety, disclosed a study on the feasibility of plasma after treatment of NOx and particulates. This study reported that although NO₂ can be used to non-thermally oxidize the carbon fraction of particulates, this does not provide a high level of reduction of NOx since it also leads to conversion of NO to NO₂.

Further, Suzanne E. Thomas, Anthony R. Martin, David Raybone, James T. Shawcross, Ka Lok Ng, Phil Beech, and J. Christopher Whitehead., “Non-Thermal Plasma After Treatment of Particulates-Theoretical Limits and Impact on Reactor Design”, SAE Paper 2000-01-1926 (2000), which is herein incorporated by reference in its entirety, disclosed work that was carried out using non-thermal plasma by introducing packing material into the plasma region to increase the residence time for the oxidation of particulate matter in the treatment of diesel exhaust. This reference showed that a non-thermal plasma reactor designed in this manner could be effective in the oxidation of particulate matter at low temperatures. This reference also reported that a two-stage plasma system might be needed to convert NO, produced during the process, back to NO₂ upstream of a catalytic treatment. This reference indicated that the plasma in combination with a catalyst would be required to take care of aldehydes and CO.

Unfortunately, each of the technologies still has one or more limitations which prevent it from providing a robust, efficient, durable, packagable, and maintenance-free, particulate trap system and method.

SUMMARY

A method for treating emissions in accordance with embodiments of the present invention includes charging particles in an exhaust stream, producing one or more radicals, oxidizing at least a portion of the charged particles with at least a portion of the produced radicals. At least a portion of the charged particles in the exhaust stream are attracted on at least one attraction surface which is one of oppositely charged from the charged particles and grounded. The attracted particles are oxidized with another portion of the one or more produced radicals to self regenerate the at least one attraction surface.

A system for treating emissions in accordance with other embodiments of the present invention includes a housing with a passage having at least one inlet and at least one outlet, at least one charging system, and at least one attraction system. The charging system charges particles in an exhaust stream in the passage, produces one or more radicals, and oxidizes at least a portion of the charged particles with at least a portion of the produced radicals. The attraction system attracts at least a portion of the charged particles in the exhaust stream on at least one attraction surface which is one of oppositely charged from the charged particles and grounded in the passage downstream from the charging system. The attracted particles on the at least one attraction surface are oxidized with another portion of the one or more produced radicals to self regenerate the attraction surface.

A method for making a system for treating emissions in accordance with other embodiments of the present invention includes providing a housing with a passage having at least one inlet and at least one outlet, providing at least one charging system, and providing at least one attraction system in the passage downstream from the charging system. The charging system charges particles in the passage, produces one or more radicals in an exhaust stream, and oxidizes at least a portion of the charged particles with at least a portion of the produced radicals. The attraction system attracts at least a portion of the charged particles in the exhaust stream on at least one attraction surface which is one of oppositely charged from the charged particles and grounded. The attracted particles on the at least one attraction surface are oxidized with another portion of the one or more produced radicals to self regenerate the attraction surface.

A corona discharge device in accordance with embodiments of the present invention includes at least one conductive member and a plurality of teeth along at least one edge of the at least one conductive member. At least one electrical connector is coupled to the at least one conductive member.

A method for making a corona discharge device in accordance with other embodiments of the present invention includes providing at least one conductive member and forming a plurality of teeth along at least one edge of the at least one conductive member. At least one electrical connector is coupled to the at least one conductive member.

A method of making corona discharge in accordance with other embodiments of the present invention includes providing at least one conductive member with a plurality of teeth along at least one edge and coupling the at least one conductive member to at least one power source. A voltage from the power source is applied to the at least one conductive member to generate an ionization discharge.

The present invention provides systems and methods for elimination of particulate matter that are robust, efficient, durable, packagable, and maintenance-free. With the present invention, air quality is improved through significant annual reductions of particulate emissions providing benefits to public health and the environment. By using non-thermal plasma, the present invention is very efficient in terms of power consumption when compared to other prior particle separation and trapping technologies. Additionally, by self oxidizing carbon particulates the present invention is able to self regenerate the catalyzed electrostatic surface. Further, the present invention provides a treatment system which has a lower weigh, and lower system pressure drop than prior units.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a partial perspective and partial broken away view of a emissions treatment system in accordance with embodiments of the present invention;

FIG. 2 is a perspective view of a corona discharge electrode device in the emissions treatment system shown in FIG. 1;

FIG. 3 is a side, perspective view of the corona probe for the corona discharge electrode device shown in FIG. 2;

FIG. 4 is a perspective view of a section of a catalyzed electrostatic system in the emission system shown in FIG. 1;

FIG. 5 is graph of experimental test results of particulate matter reduction versus corona discharge voltage;

FIGS. 6A-6C are top, perspective view of other embodiments of corona probes for the corona discharge electrode device; and

FIG. 7 is a diagram of test results of particulate matter reduction.

DETAILED DESCRIPTION

An emissions treatment system 10 in accordance with embodiments of the present invention is illustrated in FIGS. 1-4. The emissions treatment system 10 includes a housing 12 with a passage 14 having an inlet 16 and outlet 18, corona discharge electrode devices 20(1)-20(2), a catalyzed electrostatic system 22, and a catalyst system 24, although the emissions treatment system 10 can comprise other numbers and types of components in other configurations. The present invention provides a number of advantages including providing systems and methods for elimination of particulate matter which are robust, efficient, durable, packagable, and maintenance-free.

Referring to FIG. 1, the housing 12 defines the passage 14 which extends between the inlet 16 and the outlet 18, although the housing 12 could have other shapes and configurations with other numbers of passages with other numbers of inlets and outlets. The housing 12 has chambers 26(1) and 26(2) in passage 14 on opposing sides of the catalyzed electrostatic system 22, although the housing 12 could have other numbers and types of chambers in passage 14 in other configurations.

Referring to FIGS. 1-3, the corona discharge electrode device 20(1) is located in the first chamber 26(1) in the passage 14 adjacent the inlet 16, although other numbers and types of devices for charging particulate matter and in other locations could be used. The corona discharge electrode device 20(1) provides a corona discharge that is used to charge particles in an exhaust stream passing through a chamber 26(1) in the passage 14 in housing 12, such as soot in diesel exhaust.

The corona discharge electrode device 20(1) includes a ceramic base 30, a conductive rod 32, and a probe 34(1), although the corona discharge electrode device 20(1) could be comprised of other types and numbers of elements in other configurations. The base 30 is formed around and insulates the rod 32 and has a threaded end which is used to secure the base 30 in an opening in the housing 12 so the probe 34(1) is disposed in the passage 14, although other types of bases made of other materials and secured to the housing in other manners can be used and other types of conductors can be used for rod 32. In these embodiments, the probe 34(1) has an elongated, rectangular shape with teeth 35 that have sharp peaks along three sides and a smooth edge along the remaining side and the probe has a twisted configuration, although the probe 34(1) could have other numbers and type of teeth along other numbers of edges and could have other shapes in other configurations. Additionally, in this embodiment the probe 34(1) is made of brass, although other types of materials could be used.

By way of example only, other embodiments of probes 34(2)-34(4) which could be used with one or both of the corona discharge electrode devices 20(1) and 20(2) are illustrated in FIGS. 6A-6C. In this embodiment, the probe 34(2) has an elongated shape with a plurality of teeth 37 on opposing elongated sides, although the probe 34(2) could have other shapes and configurations. Each of the teeth 37 have: a sawtooth shape; substantially the same overall size; a spacing between each of the teeth 37 which is substantially the same; and a direction in which each of the teeth 37 on the same elongated side extend in substantially the same direction, although the probe 34(2) could have other types and numbers of teeth, with other spacing and direction, and with other shapes and configurations on other numbers of sides.

In this embodiment, the probe 34(3) has an elongated shape with a plurality of teeth 39 on opposing elongated sides and with an overall twisted configuration, although the probe 34(3) could have other shapes and configurations. Each of the teeth 39 have: a sawtooth shape; an overall size for each of the teeth 39 which tapers down from a center towards each of the ends of the probe 34(3); a spacing between each of the teeth 39 which is substantially the same; and a direction in which each of the teeth 39 on the same elongated side extend in substantially the same direction, although the probe 34(3) could have other types and numbers of teeth, with other spacing and direction, and with other shapes and configurations on other numbers of sides.

In this embodiment, the probe 34(4) has an elongated shape with a plurality of teeth 41 on opposing elongated sides, although the probe 34(3) could have other shapes and configurations. Each of the teeth 41 have: a sawtooth shape; substantially the same overall size; a spacing between each of the teeth 41 which is substantially the same; and a direction in which each of the teeth 41 on the same elongated side extend varies between the teeth 41, although the probe 34(4) could have other types and numbers of teeth, with other spacing and direction, and with other shapes and configurations on other numbers of sides

The different shapes, configurations, sizes and directions for the teeth on the probes 34(1)-34(4) improve the corona discharge from the corona discharge electrode devices 20(1) and 20(2). Unlike prior single pole, mesh type, or plate electrodes which serve a limited area of exhaust gas flow, the use of corona discharge electrode devices 20(1) and 20(2) with one of these probes 34(1)-34(4) leads to the formation of wide rectangular ionization field which covers a wide area of the passage 14 in housing 12.

Referring to FIG. 1, the corona discharge electrode device 20(2) is identical to the corona discharge electrode device 20(1) illustrated and described with reference to FIGS. 1-3, except as described herein. The corona discharge electrode device 20(2) is located in the second chamber 26(2) in the passage 14 between the catalyzed electrostatic system 22 and the catalyst system 24, although other numbers and types of discharge devices could be used. The corona discharge electrode device 20(2) provides a corona discharge in the chamber 26(2) in the passage 14 downstream from the catalyzed electrostatic system 22. The corona discharge is used to convert compounds in the exhaust stream, such as NO, to other compounds, such as NO₂, which can be treated by the catalyst system 24.

A high voltage power source 28 is coupled to the corona discharge electrode devices 20(1) and 20(2) and supplies power at a very high voltage between about 5 kV and 70 kV at a very low current between about 0.01 mA and 7 mA, although the power supply 28 can supply power at other voltages and currents to the corona discharge electrode device 20(1). One of the advantages of the present invention is that the system 10 works effectively with the corona discharge electrode devices 20(1) and 20(2) generating non-thermal plasma which requires less power and thus is more energy efficient.

Referring to FIGS. 1 and 4, the catalyzed electrostatic system 22 comprises a substrate core 35 which has a plurality of passages 36 that extend through, although the catalyzed electrostatic system 22 can comprise other types and numbers of components in other configurations and other types and numbers of attraction systems could be used. In this embodiment, the substrate core 35 is made of a metal with a silver coating in the passages 36, although the catalyzed electrostatic system 22 can comprise other types and numbers of components in other configurations and the substrate core and the coatings can be made of other types of materials. The catalyzed electrostatic system 22 is located in and fills the space in the passage 14 between the chambers 26(1) and 26(2) which are fluidly connected together by the passages 36, although other configurations could be used. The conductive surfaces of the catalyzed electrostatic system 22 are coupled to ground, although other types of electrically connections could be used, such as coupling the conductive surfaces of the catalyzed electrostatic system 22 to a device with an opposite charge from the charge on the particles.

The catalyzed electrostatic system 22 uses an electrostatic principal to deflect and attract charged soot particles in the exhaust stream to a surface of one of the passages 36 in the substrate core 35, although other manners for attracting the particles on other types of surfaces can be used. Additionally, the catalyzed electrostatic system 22 provides space for the conversion of soot and other particulate materials captured on the catalyzed electrostatic system 22 through oxidation so the catalyzed electrostatic system 22 can self regenerate.

Referring to FIG. 1, the catalyst system 24 includes a catalyst substrate 38 with a plurality of passages 40 and is made of a ceramic material, although the catalyst system 24 can comprise other types and numbers of components in other configurations and can be constructed with other types of materials. The catalyst system 24 is located in and fills the space of the passage 14 between the chamber 26(2) and the outlet 18 which are fluidly coupled together, although other configurations could be used. The catalyst system 24 is used to reduce or eliminate tailpipe emissions such as CO, HC and NOx with one or more reactions with catalysts in the catalyst system 24 in manners well known to those of ordinary skill in the art.

A method of reducing emissions in accordance with embodiments of the present invention will now be described with reference to FIGS. 1-4. An exhaust stream, such as diesel soot, is introduced through the inlet 16 into the chamber 26(1) in the passage 14, although other types of fluids could be introduced for treatment. Meanwhile, power supply 28 is engaged to supply power to the corona discharge electrode devices 20(1) and 20(2) in manners well known to those of ordinary skill in the art. In these embodiments, the power supplied to corona discharge electrode devices 20(1) and 20(2) is at very high voltage between about 5 kV and 70 kV with a very low current between about 0.01 mA and 7 mA, although the power can be supplied at other voltages and currents.

The high voltage applied to the corona discharge electrode device 20(1) charges carbon particles in the exhaust stream with ions repelled by the corona discharge in chamber 26(1), although other manners for charging the particulate matter in chamber 26(1) can be used. The shape and configuration of the probe 34(1) on the corona discharge electrode device 20(1) leads to the formation of an ionization field which covers a substantial portion of the chamber 26(1). The corona discharge in the chamber 26(1) also excites the gas atoms to produce highly reactive O, OH, and NO₂ radicals. These highly reactive radicals oxidize at least a portion of the soot particles passing through chamber 26(1) into gases, such as N₂, CO, CO₂ and H₂O by way of example only.

Next, the charged particles in the exhaust stream in chamber 26(1) are directed downstream into the passages 36 in the substrate core 35 of catalyzed electrostatic system 22, although the charge particles could be directed to other types of attraction systems. The charge particles in the exhaust stream migrate to and are attracted on the conductive surfaces in the passages 36 in the substrate core 35 which are coupled to ground G, although the conductive surfaces could be coupled in other manners, such as to a device which provides an opposite charge from the charge on the charge particles. By way of example only, particle migration velocities of 0.01 to 4 ft/sec are common.

Meanwhile, the radicals, such as O, OH, and NO₂, generated in the chamber 26(1) are also directed downstream into the passages 36 in the substrate core 35 in catalyzed electrostatic system 22. The radicals, such as O, OH, and NO₂, also oxidize at least a portion of the particles attracted on the conductive surfaces in the passages 36 in the substrate core 35 to self regenerate the catalyzed electrostatic system 22. These highly reactive radicals oxidize the attracted particles into gases, such as N₂, CO, CO₂ and H₂O, while again self regenerating the catalyzed electrostatic surface.

Next, the high voltage applied to the corona discharge electrode device 20(2) generates a corona discharge in chamber 26(2), although other manners for generating a corona discharge or other plasma can be used. The shape and configuration of the probe 34(1) on the corona discharge electrode device 20(2) helps to lead to the formation of the ionization field which covers a substantial portion of the chamber 26(2). The corona discharge in chamber 26(2) converts any residual compounds, such as NO, in the exhaust stream from the catalyzed electrostatic system 22 into other compounds, such as NO₂, which can be treated by the catalyst system 24, although other manners for preparing the exhaust stream in chamber 26(2) for further treatment can also be used. Yet another function occurring in chamber 26(2) with the ionization is the oxidization of at least a portion of any remaining soot particles into gases, such as N₂, CO, CO₂ and H₂O

Next, the exhaust stream is provided into the passages 40 in the catalyst substrate 38 for the catalyst system 24 to reduce or eliminate tailpipe emissions, such as CO, HC and NOx, with one or more reactions with catalysts in the catalyst system 24 in manners well known to those of ordinary skill in the art. The treated exhaust stream is then output via the outlet 18 in the housing 12, although other treatments could be applied and the exhaust could be outlet in other manners.

By way of example only, sample result from a diesel generator equipped with the system 10 is shown in FIG. 5. As illustrated, the system 10 providing a particulate matter reduction between about 37% and 80% depending upon the engine load and the level of power supplied by the power supply 28 to the corona discharge electrode devices 20(1) and 20(2). These results prove the feasibility of using non-thermal plasma with the system 10 as a viable method to reduce soot in a diesel generator and diesel engine exhaust. Additionally, by way of example only, the results from a diesel pick up truck equipped with the system 10 are also illustrated in the table shown in FIG. 7.

The present invention has a number of applications, including as a component of an emissions treatment system for automotive applications, such as off-road vehicles, distributed power systems, stationary power systems and mining systems. Other applications for the present invention, by way of example only, include removal of tar in biomass conversion and in stack gas applications.

Accordingly, the present invention provides a particulate trap system which is effective in reducing emissions, is durable, and is self-regenerating. Since the present invention works with non-thermal plasma, it is very efficient in terms of power consumption when compared to prior particle separation and trapping technologies. Another advantage of the present invention is the simplicity and effectiveness of the design of the corona probe. Yet another advantage of the present invention is the absence of precious metal such as Platinum for conversion of NO to NO₂. Yet a further advantage of the present invention is that the low temperature (>=100° C.) operation of the system 10 makes it very suitable for use in vehicles and systems, such as school busses, refuse trucks, construction equipment, on and off road vehicles, and generators by way of example only.

Having thus described the basic concept of the invention, it will be rather apparent to those skilled in the art that the foregoing detailed disclosure is intended to be presented by way of example only, and is not limiting. Various alterations, improvements, and modifications will occur and are intended to those skilled in the art, though not expressly stated herein. These alterations, improvements, and modifications are intended to be suggested hereby, and are within the spirit and scope of the invention. Additionally, the recited order of processing elements or sequences, or the use of numbers, letters, or other designations therefore, is not intended to limit the claimed processes to any order except as may be specified in the claims. Accordingly, the invention is limited only by the following claims and equivalents thereto. 

What is claimed is:
 1. A system for treating emissions, the system comprising: a housing with a passage having an inlet and an outlet; a first chamber having a lone first chamber charging system comprising a first corona discharge device which generates a non-thermal plasma that charges carbon particles in an exhaust stream in the passage with ions from the first corona discharge, excites gas atoms and produces one or more radicals, and oxidizes a portion of the charged carbon particles with a portion of the produced one or more radicals to remove a portion of the carbon particles in the exhaust stream; a flow-through maintenance-free non-charging attraction system comprising a substrate core having a plurality of individual passages that extend through from one end to the other end of the core and which fills a space in the housing passage that attracts a portion of the charged carbon particles in the exhaust stream on a conductive catalyzed attraction surface in direct contact with the plasma, which surface is at least one of oppositely charged from the charged carbon particles and grounded in the housing passage, wherein the attraction system is positioned downstream from the first chamber charging system, such that the attracted particles are resident on the attraction surface for a sufficient time to be oxidized by the non-thermal plasma with another portion of the one or more produced radicals to self regenerate the attraction surface; and a second chamber having a lone second chamber charging system comprising a second corona discharge device which generates a non-thermal plasma that oxidizes a portion of the charged carbon particles with ions from the second corona discharge and converts residual compounds from the first chamber into other compounds capable of treatment by a catalyst system and a non-charging flow-through catalyst system comprising a substrate having a plurality of individual passages that extend therethrough and which fills a space of the housing passage between the second chamber and the outlet that catalyzes the other compounds from the second chamber to reduce or eliminate emissions from the exhaust stream.
 2. The system as set forth in claim 1 wherein the produced one or more radicals comprises at least one of O, OH, and NO₂.
 3. The system as set forth in claim 1 wherein the portion of removed carbon particles are removed from the exhaust stream by the first corona discharge device by being oxidized into gases comprising at least one of N₂, CO₂, and H₂O.
 4. The system as set forth in claim 1 wherein the attracted particles on the attraction surface are oxidized into gases comprising at least one of N₂, CO, CO₂, and H₂O to self regenerate the attraction surface.
 5. The system as set forth in claim 1 wherein charged carbon particles are removed from the exhaust stream by the second corona discharge device by being oxidized into gases comprising at least one of N₂, CO₂, and H₂O.
 6. The system as set forth in claim 1 wherein the second charging system converts the residual compounds from the first chamber into other compounds by converting at least a portion of nitrogen oxide in the exhaust stream to nitrogen dioxide.
 7. The system as set forth in claim 1 wherein the other compounds from the second chamber reduced or eliminated from the exhaust stream are emissions comprising at least one of CO, HC, and NO_(x).
 8. A method for making a system for treating emissions, the method comprising: providing a housing with a passage having at least one inlet and at least one outlet; providing a first chamber having a lone first chamber charging system comprising a first corona discharge device which generates a non-thermal plasma that charges carbon particles in an exhaust stream in the passage with ions from the first corona discharge, excites gas atoms and produces one or more radicals in the exhaust stream, and oxidizes a portion of the charged carbon particles with a portion of the produced one or more radicals to remove a portion of the carbon particles in the exhaust stream; providing a flow-through maintenance-free non-charging attraction system comprising a substrate core having a plurality of individual passages that extend through from one end to the other end of the core and which fills a space in the housing passage downstream from the charging system, the attraction system attracts at least a portion of the charged carbon particles in the exhaust stream on a conductive catalyzed attraction surface in direct contact with the plasma, which surface is at least one of oppositely charged from the charged carbon particles and grounded, such that the attracted particles are resident on the attraction surface for a sufficient time to be oxidized by the non-thermal plasma with another portion of the one or more produced radicals to self regenerate the attraction surface; and a second chamber having a lone second chamber charging system comprising a second corona discharge device which generates a non-thermal plasma that oxidizes a portion of the charged carbon particles with ions from the second corona discharge and converts residual compounds from the first chamber into other compounds capable of treatment by a catalyst system and a non-charging flow-through catalyst system comprising a substrate having a plurality of individual passages that extend therethrough and which fills a space of the housing passage between the second chamber and the outlet that catalyzes the other compounds from the second chamber to reduce or eliminate emissions from the exhaust stream.
 9. The method as set forth in claim 8 wherein the produced one or more radicals comprises at least one of O, OH, and NO₂.
 10. The method as set forth in claim 8 wherein the portion of removed carbon particles are removed from the exhaust stream by the first corona discharge device by being oxidized into gases comprising at least one of N₂, CO₂, and H₂O.
 11. The method as set forth in claim 8 wherein the attracted particles on the attraction surface are oxidized into gases comprising at least one of N₂, CO, CO₂, and H₂O to self regenerate the attraction surface.
 12. The method as set forth in claim 8 wherein charged carbon particles are removed from the exhaust stream by the second corona discharge device by being oxidized into gases comprising at least one of N₂, CO₂, and H₂O.
 13. The method as set forth in claim 8 wherein the second charging system converts the residual compounds from the first chamber into other compounds by converting at least a portion of nitrogen oxide in the exhaust stream to nitrogen dioxide.
 14. The method as set forth in claim 8 wherein the other compounds from the second chamber reduced or eliminated from the exhaust stream are emissions comprising at least one of CO, HC, and NO_(x). 